Conductive masterbatches and conductive monofilaments

ABSTRACT

The present invention relates to a polyester matrix powder comprising a polybutylene terephthalate, a homogeneously dispersed carbon nanotube powder, a dispersant and a chain extender; to a conductive masterbatch with homogeneous and smooth surface; to a process for the preparation of the conductive masterbatch; to a conductive monofilament prepared from the conductive masterbatch; to a process for the preparation of the conductive monofilament; and to a fabric article prepared from the monofilament. The present invention is characterized in the preparation of carbon nanotube-containing fiber materials with higher conductivity and the improvement of the spinning property of the conductive masterbatches to avoid blocking and yarn breakage during the spinning process.

RELATED APPLICATIONS

This application is a Divisional patent application of co-pendingapplication Ser. No. 12/346,104, filed on 30 Dec. 2008, now pending. Theentire disclosure of the prior application Ser. No. 12/346,104, fromwhich an oath or declaration is supplied, is considered a part of thedisclosure of the accompanying Divisional application and is herebyincorporated by reference.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to polyester matrix powders containingcarbon nanotube powders dispersed therein; to conductive masterbatcheswith homogeneous and smooth surfaces and the preparing process thereof;to conductive monofilaments formed from the said conductivemasterbatches and the preparing process thereof; and to textilesprepared from the said conductive monofilaments.

2. Description of Related Arts

Carbon nanotubes have been known as graphitizing carbon tubes and aredifferent from conventional carbons in that the carbon nanotubes have aspecific character of L/D ratio and can be used as the best conductivematerials. Generally, the larger the L/D ratio of carbon nanotubes is,the better the conductivity of the same is. However, if the L/D ratio istoo large, problems occur during spinning process. For instance, if thearrangement or orientation of the carbon nanotubes is not good, thedrawing process becomes difficult. Further, if the carbon nanotubes failto pass the fiber filter test, the filaments formed therefrom easilybreak during spinning process.

In order to enhance the conductivity of polymer matrixes, carbonnanotubes having good dispersibility may be added. The carbon nanotubesare obtainable by a high-speed mechanic force, followed by uniformlydispersing the carbon nanotubes in the polymer matrixes. However,achieving the dispersing effect and enhancing the conductivity of thepolymer matrixes via such a high-speed mechanic process are onlyeffective when the concentration of carbon nanotubes is low. If theconcentration of the carbon nanotubes is high, the uniform dispersingeffect cannot be reached even though the conductivity is increased. Onthe other side, the longer the carbon nanotubes is, the better theincreasing effect of their conductivity is. Nevertheless, if the longlength of the carbon nanotubes is disadvantageous to the processability.Such a result is caused by the tanglement of the carbon nanotubesthemselves.

Recently, the high-speed shear mixing and processing technology makesthe addition of up to 15 wt. % of the carbon nanotubes in the polymermatrix possible. However, the carbon nanotubes have poor dispersibilityin the polymer materials by their process.

In other conventional methods, carbon nanotubes are dispersed in astrong acid solution to shatter the aggregates of the carbon nanotubesvia ultrasonic wave. Specifically, the aggregates may be shattered in amixed acid solution containing H₂SO₄ and HNO₃ in a ratio of 3:1 at 50°C. via ultrasonic wave over a time period of 24 hours. The carbonnanotubes treated by a strong acid solution are easy to produce a COOHgroup that may increase the dispersibility of carbon nanotubes. However,this method has disadvantages in that the carbon nanotubes treated by astrong acid solution cause defects on the surfaces of their structures,and thus the properties and functions of the carbon nanotubes will begreatly reduced.

The prior art, for instance, CN1475437A discloses a process for thepreparation of a carbon nanotube paper, comprising the steps of:purifying carbon nanotubes, dispersing the carbon nanotubes and forminga carbon nanotube paper; wherein the carbon nanotubes are repeatedlytreated until the impurities are removed and the carbon nanotubes aresufficiently dispersed. Such processes have several disadvantages, suchas: 1) the procedure is very complicated and costly; 2) the surfaces ofcarbon nanotubes treated with a strong acid will be destroyed and theproperties, such as antistatic ability, conductivity or strength, of thecarbon nanotubes become poor; 3) it is difficult to disperse the carbonnanotubes in a solvent and the solvent used causes an environmentalproblem; and 4) the surfaces of the carbon nanotubes are destroyed dueto the treatment with a strong acid and the yield is only about 30 to60%, whereby the production cost of the carbon nanotubes issignificantly increased.

CN1563526A discloses conductive fibers containing carbon nanotubes andthe preparing process thereof. The conductive fibers comprise 80 to 99.9wt. % of a polyester, 0.05 to 10 wt. % of carbon nanotubes and 0.05 to10 wt. % of a coupling agent, wherein the coupling agent is selectedfrom OP wax, montan wax, polyethylene vinyl acetate or aluminate. Inthis known technology, the carbon nanotubes are untangled under a strongshear force, thereby being homogeneously dispersed within the polyestermatrix. In this process, only a lower content of carbon nanotubes isrequired for preparing conductive fibers. According to this process, thecoupling agent is added after the polyester and carbon nanotubes aredried under vacuum, followed by mixing them at a high speed and at atemperature of 70 to 120° C. After that, masterbatches are prepared at aspeed of 40 to 150 rpm by using a twin-screw mixer. According to thisprocess, it is difficult to untangle the carbon nanotubes due to thelong length L (=100 μm) of carbon nanotubes, as shown in the examples ofthis China application. Thus, filaments formed from the said carbonnanotubes fail to pass the filter test and possibly break duringspinning process. Furthermore, due to the coupling agent and low contentof the carbon nanotubes, the increase of the conductivity of thefilaments formed according to such a process is limited. In addition,the carbon nanotubes are drawn out during the vacuum dryness procedurefor the polyester and carbon nanotubes, and the conductivity of thecarbon nanotubes is reduced because of the low content of carbonnanotubes. The masterbatches from the carbon nanotubes prepared by thisprocess exhibit poor physical properties. It is necessary to usebi-component composite spinning method to produce filaments. Moreover,the conductivity of the filaments is lowered and the textiles preparedtherefrom merely exhibit an antistatic effect and have a surfaceresistance of 1.2×10⁶ Ω/sq.

Further, CN1584141A discloses conductive composite fibers colored withoriginal liquid by composite spinning process, characterized in that thefibers are composed of a core layer and a sheath layer, wherein the corelayer is a polyester containing 2 to 60% of conductive componentsselected from a conductive carbon black, a carbon nanotube, anano-graphite or conductive metal oxides, which has a surface resistanceof less than 10⁶ Ω·cm. The process of this China application comprisesdispersing the conductive particles by melt-state mixing. Themasterbatches formed from the carbon nanotube according to this processhave unstable physical properties. Thus, it is necessary to use abi-component spinning procedure to enhance the mechanical properties offibers.

CN1869291A discloses a fiber structure of nano compound materialcontaining a polyester and a carbon nanotube, wherein the polyester andcarbon nanotube are dispersed in a solvent to form a stable dispersioncontaining polyester/carbon nanotube, and then a fiber structure of nanocompound material containing a polyester and a carbon nanotube, such asthe structures of a fiber and a non-woven fabric or film formedtherefrom is prepared by electrostatic spinning. The formed fiber ornon-woven fabric or film has a conductivity of 10⁻¹⁷ to 10² S/cm. Inthis process, the carbon nanotube is dispersed in the polyester byultrasonic or mechanical or electromagnetic stirring step.

U.S. Pat. No. 7,094,467B2 discloses an antistatic polymer monofilamentand the preparing process thereof. The antistatic polymer monofilamentcomprises a polymer composite of a thermoplastic polymer as a matrix andcarbon nanotubes as a conductive filler. The textiles formed from themonofilament have a surface resistance of 10⁴ to 10⁹ ω/sq. However, thetextiles only exhibit an antistatic effect and haves a surfaceresistance of 2×10⁷ ω/sq.

In the conventional technology, carbon nanotubes is generally added inthe polymer in an amount of 2 wt. % or less. Such an amount of thecarbon nanotubes limits the increase of the conductivity. It is knownthat the dispersibility of the carbon nanotubes is poor and may resultin breakage, brittleness and difficulties in granulating the polymermatrix when the carbon nanotubes in the polyester matrix are in anamount of 5 wt. % or more. The problems and disadvantages stated abovemay be solved by the addition of a dispersant and a chain extender.

Accordingly, in order to obtain conductive monofilaments containing alow content of carbon nanotubes and having good conductivity andexcellent spinning processability as well as to avoid theabove-mentioned disadvantages and problems, the present inventionprovides novel conductive polyester materials, which comprises polyestermatrix powders containing a homogeneously dispersed carbon nanotube, adispersants and a chain extender.

SUMMARY OF THE INVENTION

The object of the present invention is to provide polyester matrixpowders containing carbon nanotube powders dispersed therein and havingexcellent electrical conductivity, the applications of conductivemasterbatches, conductive monofilamens and textiles, and the processesfor preparation of the same.

DETAILED DESCRIPTION OF THE INVENTION

The present invention provides a polyester matrix powder containingcarbon nanotube powders homogeneously dispersed therein, wherein thepolyester matrix powder comprises:

-   A) a polyester polymeric matrix based on polybutylene    terephthalate(PBT) or the copolymers thereof,-   B) carbon nanotube powders which have been milled at a ultrahigh    speed,-   C) a dispersant, and-   D) a chain extender,    wherein the above components A), B), C) and D) are mixed in a    high-speed powder mixer, to obtain a polyester matrix powder.

For component A) of the present invention, polybutylene terephthalate orthe copolymer thereof is selected from the group consisting ofpolybutylene terephthalate homopolymer, copolyester containing butyleneterephthalate (BT) as the repeat unit and block copolymer containingpolybutylene terephthalate, or the combination thereof. Polybutyleneterephthalate homopolymer is preferred.

According to one embodiment of the present invention, the polybutyleneterephthalate or the copolymer thereof has an intrinsic viscosity (I.V.)of 0.6 dl/g or more. Preferably, the intrinsic viscosity (I.V.) is in arange of 0.8 to 1.3 dl/g, determined in 50/50 (v/v) oftetrachloroethane/phenol at 25° C.

In this invention, the content of the component A) is 80 to 99.5 wt. %,preferably 84 to 99 wt. %, more preferably 88 to 97 wt. %, based on theweight of polyester matrix powder.

Suitable carbon nanotube in the present invention has a purity of 90%and is milled by means of an ultrahigh-speed powder pulverizer to form adispersed carbon nanotube powder. According to a preferred embodiment ofthe present invention, the carbon nanotube powder is milled by means ofa powder pulverizer at a speed of 20,000 to 30,000 rpm for 5 to 20minutes, thereby forming a carbon nanotube powder with a gooddispersibility and having a length (L) of less than 3.0 μm (micrometer)and a L/D value of greater than 100. Preferably, the carbon nanotubepowder after milling has a length (L) of 0.7 to 3 μm and a L/D value of100 to 300.

According to an embodiment of the present invention, the carbon nanotubecontained in the carbon nanotube powder has an average diameter of 0.5to 50 nm (nanometer) and an L/D value of 60 to 600.

The content of carbon nanotube powder according to the present inventionis 1 to 15 wt. %, preferably 1 to 10 wt. %, more preferably 2.5 to 10wt. %, and most preferably 3 to 10 wt. %, based on the weight ofpolyester matrix powder.

The polyester matrix powder of the present invention contains adispersant as component C). The dispersant exhibits processing stabilityand functions of improved dispersibility and flowability. During theprocessing process, the dispersant may produce a free radical thatcombines the carbon nanotube with the dispersant. Suitable dispersantused in the present invention is an ethylene-acrylic copolymer.According to one preferred embodiment of the present invention, thedispersant is ethylene-acrylic acid copolymer.

The content of the dispersant in the present invention is 0.01 to 6.0wt. %, preferably 0.1 to 2.0 wt. %, more preferably 0.2 to 1.5 wt. %,based on the weight of polyester matrix powder.

In the present invention, to reinforce the processing ability of thepolyester fiber, such as size stability, thermal stability, etc., achain extender as component D) may be added. The smaller molecular chainsegment in the polymer is extended to form longer one by the combinationof the unique functional group in the chain extender with the smallermolecular chain segment, i.e. carboxyl group (—COOH), thereby enhancingthe properties of the materials, such as intrinsic viscosity (I.V.),thermal stability, size stability, etc. and avoiding the influence ofthe high-temperature mixing and spinning processes on the physicalproperties of the materials.

According to the present invention, suitable chain extender is selectedfrom the group consisting of a diisocyanatocycloalkane or an oxazoline.The exemplary compounds are diisocyanatocycloalkane of formula (I),

bis-oxazoline of formula (II),

1,4-phenylene-bis-oxazoline,

2,2′-methylene bis[(4S)-4-tert-butyl-2-oxazoline] of formula (IV),

2,2′-methylene bis[(4S)-4-phenyl-2-oxazoline] of formula (V),

The content of the chain extender in the present invention is 0.01 to6.0 wt. %, preferably 0.1 to 1.0 wt. %, more preferably 0.1 to 0.8 wt.%, based on the weight of polyester matrix powder.

According to the present invention, A) a polyester polymeric matrix, B)a carbon nanotube powder milled at ultrahigh speed, C) a dispersant andD) a chain extender are mixed by means of a solid dispersing andblending technology. According to one embodiment of the presentinvention, the carbon nanotube powder is quickly and homogeneouslydispersed in the polyester polymeric matrix in a high-speed powder mixerat a speed of 1,000 to 3,000 rpm for 10 to 60 minutes to obtain apolyester matrix powder containing a homogeneously dispersed carbonnanotube powder.

Accordingly, one further object of the present invention is to provide aprocess for the preparation of a polyester matrix powder containing ahomogeneously dispersing carbon nanotube, characterized in that theprocess comprises the steps of:

-   1) providing a carbon nanotube with a purity of more than 90% and    having a length (L) of less than 2 μM and a L/D value of more than    100,-   2) feeding the carbon nanotube into a ultrahigh-speed powder    pulverizer at a speed of 20,000 to 30,000 rpm to mill the carbon    nanotube for 5 to 20 minutes to form a carbon nanotube powder with    good dispersibility,-   3) adding the dispersed carbon nanotube powder obtained from step 2)    into a polybutylene terephthalate polymeric material and then adding    a dispersant and a chain extender to form a polyester matrix    mixture,-   4) feeding the polyester matrix mixture into a high-speed powder    mixer and mixing the mixture at a speed of 1,000 to 3,000 rpm for 10    to 60 minutes to quickly and homogeneously dispersing the carbon    nanotube powder in the polyester matrix mixture, thereby forming a    polyester matrix powder containing a homogeneously dispersing carbon    nanotube.

Suitable carbon nanotube used in the process of the present inventionhas a purity of more than 90%. The carbon nanotube after milling has alength (L) of less than 3.0 μM and an L/D value of more than 100.According to one embodiment of the process of the present invention, thecarbon nanotube after milling has a length (L) of 0.7 to 2.0 μm and anL/D value of 100 to 300. According to a preferred embodiment of thepresent invention, the carbon nanotube in the carbon nanotube powder hasan average diameter of 0.5 to 50 nm and an L/D value of 60 to 600.

In the process of the present invention, suitable polybutyleneterephthalate (PBT) polymer matrix is selected from the group consistingof a polybutylene terephthalate or the copolymers thereof. Preferably,the polymer matrix is selected from the group consisting of apolybutylene terephthalate homopolymer, a copolyester containingbutylene terephthalate (BT) as the repeat unit and a block copolymercontaining polybutylene terephthalate unit, or the combination thereof.The polybutylene terephthalate homopolymer is preferred. According toone preferable embodiment of the present invention, polybutyleneterephthalate or the copolymers thereof has an intrinsic viscosity(I.V.) of more than 0.6 dl/g, preferably an intrinsic viscosity (I.V.)of 0.8 to 1.3 dl/g, determined in 50/50 (v/v) oftetrachloroethane/phenol at 25° C.

In the process of the present invention, the dispersant may be theone(s) having an improved processing stability, dispersibility andflowability, such as ethylene-acrylic copolymer. The preferabledispersant is ethylene-acrylic acid copolymer.

In the process of the present invention, the chain extender is selectedfrom the group consisting of a diisocyanatocycloalkane and an oxazoline.As stated above, the exemplary chain extender is diisocyanatocyclohexaneof formula (I), bis-oxazoline of formula (II),1,4-phenylene-bis-oxazoline of formula (III), 2,2′-methylenebis[(4,s)-4-tert-butyl-2-oxazoline] of formula (IV) or 2,2′-methylenebis[(4,s)-4-phenyl-2-oxazoline] of formula (V). Preferably, the chainextender is bis-oxazoline of formula (II), 1,4-phenylene-bis-oxazolineof formula (III), 2,2′-methylene bis[(4,s)-4-tert-butyl-2-oxazoline] offormula (IV) or 2,2′-methylene bis[(4,s)-4-phenyl-2-oxazoline] offormula (V).

The polyester matrix powder obtained by the above process may further beprocessed and mixed to form electrically conductive masterbatches.

Thus, the further object of the present invention is to provideconductive masterbatches with homogeneous and smooth surfaces,characterized in that the conductive masterbatches are obtained from thepolyester matrix powder which is prepared by mixing and granulation viatwin-screw mixer according to the process of the present invention, toform conductive masterbatches with homogeneous and smooth surfaces.

According to an embodiment of the present invention, the polyestermatrix powder is mixed and granulated by means of twin-screw mixer at atemperature of 220 to 300° C., preferably 230 to 285° C., and at a screwspeed of 300 to 400 rpm, preferably 200 to 350 rpm, more preferably 350rpm.

In the present invention, the obtained conductive masterbatches may passa filter test, such as 60 μm-screen filter test. According to anembodiment of the present invention, the formed conductive masterbatcheshave a resistance of less than 10⁸ Ω/sq, preferably 10° to 10⁸ Ω/sq,more preferably 10° to 10⁵ Ω/sq, most preferably 10¹ to 10⁴ Ω/sq, andvery preferably 10¹ to 10³ Ω/sq.

The further one object of the present invention is to provide a processfor the preparation of conductive masterbatches with homogeneous andsmooth surfaces, wherein the process comprises the steps of:

-   1) providing a polybutylene terephthalate (PBT) polymeric matrix    powder comprising a carbon nanotube powder with good dispersibility,    a dispersant and a chain extender, wherein the carbon nanotube is    milled in a ultrahigh-speed powder grinder to form a homogeneously    dispersed carbon nanotube powder before the addition to the PBT    polymer material,-   2) feeding the PBT polymeric matrix powder into twin-screw mixer and    mixing and granulating the powder at a temperature of 220 to 300°    C., preferably 230 to 285° C., and at a screw speed of 300 to 400    rpm, preferably 200 to 350 rpm, more preferably 350 rpm, thereby    forming conductive masterbatches with homogeneous and smooth    surfaces.

The present invention is further to provide a conductive monofilamentprepared from the conductive masterbatches obtained by the process ofthe present invention via spinning procedure.

The conductive monofilament formed according to the present inventionhas a diameter of 0.05 to 1.0 mm, preferably 0.1 to 0.5 mm. According tothe present invention, the conductive monofilament has a volume specificresistance of 10⁴ Ω·cm or less, preferably 10³ Ω·cm or less, and morepreferably 10¹ to 10³ Ω·cm. The conductive monofilament formed accordingto the present invention has a strength of more than 0.8 gf/d,preferably 1.0 to 4.0 gf/d, more preferably 1.0 to 2.0 gf/d. Further,the conductive monofilament formed according to the present inventionhas an elongation of more than 10%, preferably 10 to 100%, morepreferably 10 to 70%.

Further, the present invention provides a process for the preparation ofthe conductive monofilament, comprising the steps of:

-   1) providing conductive masterbatches formed from a polybutylene    terephthalate (PBT) polymer matrix powder which contains a dispersed    carbon nanotube powder, a dispersant and a chain extender, wherein    the carbon nanotube powder is homogeneously dispersed in the polymer    matrix powder,-   2) baking and drying the conductive masterbatches at 110° C. over a    time period of 12 hours to obtain dried conductive masterbatches,-   3) feeding the dried conductive masterbatches into a single-screw    and extruding the masterbatches through a 60 μm-screen filter at a    processing temperature of 250 to 285° C. and at a screw speed of 20    rpm, followed by spinning via a spinning nozzle with a pore diameter    of 0.5 mm and a length of 1 mm at a single-pore extruding rate of 6    g/minutes to form a filament,-   4) cooling the spun filament via a cooling device at a cooling rate    of 10 to 30 m/minutes, and then winding the filament at a winding    rate of 40 to 100 m/minutes to form a conductive monofilament.

The present invention further provides textiles obtained from theconductive monofilament by processing and shaping procedures, whereinthe textiles have a surface resistance of less than 10⁵ Ω/sq, preferably10¹ to 10⁵ Ω/sq.

The present invention is characterized in that the carbon nanotubepowder is dispersed and the carbon nanotube powder is untangled by meansof a ultrahigh-speed, high-strength mechanical force. The advantages ofthe process according to the present invention is simple, quick,low-cost and free of environmental problems as well as the yield of morethan 95% for the carbon nanotube.

According to the present invention, the obtained polyester matrix powdercontaining homogeneously dispersed carbon nanotube powder is suitablefor the preparation of conductive polymer masterbatches with homogeneousand smooth surfaces, of conductive monofilament (such as antistatic orconductive monofilament or multifilament), etc. Further, the conductivemonofilament prepared according to the process of the present inventionis suitable for the preparation of textiles, such as textiles forfiltration, a brush for electronic devices, a running belt, a deliveringbelt, a packaging material, a clean room or ESD (such as petrochemicalindustry, aircraft industry, explosive, spraying paint, etc.) or ananti-electromagnetic wave EMI, etc., a dust-proof cloth and anantistatic product (such as antistatic/conductive cloth,anti-electromagnetic cloth, antistatic/conductive groove,antistatic/conductive woven belt, antistatic shoe material, antistaticpackaging material, antistatic furniture cloth/carpet, etc.)

In the present invention, the percentage shown in the presentdescription and claims refers to a percentage based on the weight,unless indicated otherwise. The invention is illustrated in greaterdetail by the examples described below. The examples are not intended inany way to limit the scope of the invention. Notwithstanding that thenumerical ranges and parameters setting forth the broad scope areapproximations, the numerical values set forth in the specific exampleare reported as precisely as possible. Any numerical value, however,inherently contains certain errors necessarily resulting from thestandard deviation found in its respective testing measurements. Thepresent invention is now to be explained in more detail with the aid ofthe following examples.

EXAMPLES

A. Types and Characters of Materials

1. Polybutylene terephthalate(PBT) has an intrinsic viscosity (I.V.) of1.0 dl/g, determined in 50/50 (v/v) of tetrachloroethane/phenol at 25□.Trademark Name: 1100M, available from Changchun Group.

2. Carbon nanotube (CNT) powder, Trademark Name: Nanocyl 7000 availablefrom Nanocyl S.A., Belgian, has an average diameter of 9.5 nm, anaverage length of 1.5 μm, a length/diameter ratio (L/D) value of 158, acarbon-containing purity of 90% and a specific surface area of 250 to300 m²/g.

3. Dispersant is, Trademark Name: Wax series A-C 540A available fromHoneywell, ethylene-acrylic acid copolymer having a melting point of105° C.

4. Chain extender is a compound of 2,2′-methylenebis[(4,s)-4-phenylene-2-oxazoline], available from ShanghaiCrystalline-Purifying Regent, Ltd.

B. Device Models

1. Ultrahigh-speed, high-strength mechanical device is used fordispersing carbon nanotube, Device Model: Model RT-08 grinder with aspeed of 20,000 to 30,000 rpm, available from Mill Powder Tech Solution.

2. High-speed complex powder blending grinder is for homogeneouslydispersing carbon nanotube within polymeric material, Device Model:Model FM-20 device having a speed of 1,000 to 3,000 rpm, available fromMitsuiMining Co., Ltd. (Japan).

3. Twin-screw mixer/Twin-screw extruder is available from HAAKE(Germany).

4. Polymer melt filter device/Filter screen test device for elevatingthe distribution of carbon nanotube is a device having a 60 μm offiltering screen, available from HAAKE (Germany).

5. The main device of monofilament spinner is available from HAAKE(Germany), wherein the spinning nozzle has a pore diameter of 0.5 mm, alength of 1 mm, and the upper of the spinning nozzle is equipped with afiltering screen having a diameter of 60 μm for filtering impurities andfor enhancing the stability and quality of the spun fiber.

C. The Property Testing of Masterbatches and Fibers

1. Testing for the conductivity of conductive PBT masterbatches

PBT masterbatches are heated and melted, and then pressed to form asquare sample with 5 cm×5 cm and a thickness of about 1 mm. Theconductivity, i.e. surface resistance (Ω/sq), of the samples isdetermined by using a 4-pin probe low resistivity meter (Model:MCP-T600, available form Mitsubishi Chemical (Japan)).

2. Testing for the Conductivity of Conductive PBT Monofilament

The conductivity of PBT monofilament is determined by standard method ofDIN 54345, wherein the testing distance is 10 cm. The determinedresistance is divided by 10 cm to calculate a fiber resistivity (Ω/cm),followed by multiplying the fiber resistivity by the section area of thefiber to yield the volume specific resistance (Ω·cm) of fiber.

3. Testing for the Conductivity of Textiles Prepared from PBTMonofilament

The conductivity of the textiles prepared from PBT monofilament isdetermined by using the standard method of EN 1149-1: 1996 at atemperature of 23±1° C. and a humidity of 25±5% by means of a surfaceresistance determining meter.

4. Testing for the Rise of Pressure

The rise of pressure is determined by using a pressure testing deviceavailable from HAAKE (Germany) with a 60 μm of filtering screen for thefilter testing of conductive masterbatches.

5. Evaluation of Spinnability

The spinning test of the conductive fiber is carried out by using amonofilament spinner available from HAAKE (Germany) at a spinningtemperature of 250 to 285° C. and at a screw speed of 20 rpm to evaluatewhether the filament breaks.

6. Testing for the Properties of the Tensile Strength, Force andElongation of the Conductive Monofilament

The force, strength and elongation of the conductive monofilament aredetermined by using a Tensile strength testing machine available fromGotech Testing Machines Inc. (Taiwan) at an ambient temperature of 25°C., a distance of 250 mm between carriers, a tensile speed of 250mm/minutes. The Maximum force of breaking the filament refers to theforce of monofilament. The strength of the monofilament is obtained fromthe force of the filament divided by the danier number of the filament.The elongation of monofilament is obtained from the result of theelongation at break divided by the distance of 250 mm.

A. Preparation of Polyester Matrix Powders Containing Dispersed CarbonNanotubes

Comparative Example 1 (C. Ex. 1)

Polybutylene terephthalate(PBT) polymeric matrix is fed into ahigh-speed composite powder mixer and is mixed at a speed of 2000 rpmover a time period of 30 minutes to obtain a PBT polyester matrix powderas the control.

Comparative Example 2 (C. Ex. 2)

1932 g (96.60%) of polybutylene terephthalate (PBT) polymeric material,60 g (3.00%) of Nanocyl 7000 carbon nanotube, 4 g (0.20%) of A-C 540A asa dispersant and 4 g (0.20%) of2,2′-methylene[(4,s)-4-phenyl-2-oxazoline] are mixed to obtain PBTpolyester matrix powder as a control containing carbon nanotube powder,where the Nanocyl 7000 carbon nanotube in this comparative example isdispersed and mixed without using a ultrahigh-speed, highly strong forceand without using a high-speed, highly strong mechanical force.

Comparative Example 3 (C. Ex. 3)

Analogously to Comparative Example 2, 1870 g (93.50%) of polybutyleneterephthalate (PBT) polymeric material, 120 g (6.00%) of Nanocyl 7000carbon nanotube, 6 g (0.30%) of A-C 540A dispersant and 4 g (0.20%) of2,2′-methylene[(4,s)-4-phenyl-2-oxazoline] are mixed to obtain PBTpolyester matrix powder containing carbon nanotube powder.

Comparative Example 4 (C. Ex. 4)

1870 g (93.50%) of polybutylene terephthalate(PBT) polymeric material,120 g (6.00%) of Nanocyl 7000 carbon nanotube, 6 g (0.30%) of A-C 540Adispersant and 4 g (0.20%) of 2,2′-methylene[(4,s)-4-phenyl-2-oxazoline]are mixed. The obtained PBT polymeric matrix mixture is fed into ahigh-speed compounding powder mixer and mixed at a speed of 2000 rpm for30 minutes to obtain PBT polyester matrix powder containing carbonnanotube powder. The Nanocyl 7000 carbon nanotube in this comparativeExample was dispersed without using ultrahigh-speed, highly strongmechanical force.

Comparative Example 5 (C. Ex. 5)

Nanocyl 7000 carbon nanotube is fed into an ultrahigh-speed powdergrinder and milled at a speed of 30000 rpm for 5 minutes to form acarbon nanotube powder with good dispersibility.

120 g (6.00%) of the carbon nanotube powder and 6 g (0.30%) of A-C 540Adispersant are added to 1874 g (93.70%) of polybutylene terephthalate(PBT) polymeric matrix and mixed to obtain a PBT polyester mixture.Then, the polyester mixture is fed into a high-speed composite powdermixer and mixed at a speed of 2000 rpm for 30 minutes in order toquickly and homogeneously dispersing the Nanocyl 7000 carbon nanotubepowder in the PBT polyester matrix, thereby obtaining PBT polyestermatrix powder containing homogeneously dispersed carbon nanotube powder.In this Comparative Example, the polyester matrix powder contains nochain extenders.

Example 1 (Ex. 1)

Nanocyl 7000 carbon nanotube is fed into an ultrahigh-speed powdergrinder and milled at a speed of 30000 rpm for 5 minutes to form acarbon nanotube powder with good dispersibility.

20 g (1.00%) of the carbon nanotube powder, 2 g (0.10%) of A-C 540Adispersant and 2 g (0.10%) of 2,2′-methylene[(4,s)-4-phenyl-2-oxazoline]are added to 1976 g (98.80%) of polybutylene terephthalate (PBT)polymeric matrix and mixed to obtain a PBT polyester mixture. Then, thepolyester mixture is fed into a high-speed composite powder mixer andmixed at a speed of 2000 rpm for 30 minutes in order to quickly andhomogeneously dispersing Nanocyl 7000 carbon nanotube powder in PBTpolyester matrix, thereby obtaining a PBT polyester matrix powdercontaining homogeneously dispersed carbon nanotube powder.

Examples 2 to 6 (Ex. 2 to Ex. 6)

Analogously to Example 1, the PBT polyester matrix powder of Examples 2to 6 containing homogeneously dispersed carbon nanotube powder areprepared according to the composition ratios shown on table 1.

TABLE 1 CNT (Nanocyl 7000) Dispersing Dispersing without with high-high-speed, speed, highly Chain highly strong strong me- Dispersantextender, PBT, g mechanic chanic force, A-C540A, g (wt. %) force, g (wt.%) g (wt. %) g (wt. %) (wt. %) Controls C. Ex. 1 2000 — — — —   (100%) —— — — C. Ex. 2 1932 60 —  4 4 (96.60%) (3.00%) — (0.20%) (0.20%) C. Ex.3 1870 120 —  6 4 (93.50%) (6.00%) — (0.30%) (0.20%) C. Ex. 4 1870 120 — 6 4 (93.50%) (6.00%) — (0.30%) (0.20%) C. Ex. 5 1874 — 120  6 —(93.70%) —  (6.00%) (0.30%) — According to the present invention Ex. 11976 —  20  2 2 (98.80%) —  (1.00%) (0.10%) (0.10%) Ex. 2 1932 —  60  44 (96.60%) —  (3.00%) (0.20%) (0.20%) Ex. 3 1970 — 120  6 4 (93.50%) — (6.00%) (0.30%) (0.20%) Ex. 4 1968 — 120  8 4 (93.40%) —  (6.00%)(0.40%) (0.20%) Ex. 5 1824 — 160 12 4 (91.20%) —  (8.00%) (0.60%)(0.20%) Ex. 6 1775 — 200 20 5 (88.75%) — (10.00%) (1.00%) (0.25%)B. Preparation and Property Testing for Conductive Masterbatches

Each of PBT polymeric matrix powders prepared by Comparative Example 1to 5 and Examples 1 to 6 is fed into a twin-screw mixer and then mixedand granulated at a temperature of 230 to 300° C. and a screw speed of350 rpm to prepare conductive masterbatches.

The masterbatches obtained from Comparative Example 1 to 5 and Example 1to 6 respectively refer to as sample Nos.: C-PBT, PCN3-0, PCN6-1,PCN6-2, PCN6-3, PCN1-1, PCN3-1, PCN6-4, PCN6-5, PCN8-5 and PCN10-1, andthe dispersibility of the carbon nanotube are evaluated by using afilter screen testing machine, available from HAAKE (Germany), with a 60μm screen. Dispersibility is evaluated by the determination of thepressure rise in the filter test and the result is shown on table 2.

TABLE 2 Dispersing PBT + CNT (Nanocyl 7000) CNT + dispersant +Dispersing chain extender with The distribution of CNT in withoutDispersing with high-speed, highly polymeric matrix ultrahigh-speed,ultrahigh-speed, strong mechanic force change of Evaliation PBT highlystrong highly strong (high-speed Surface preessure of Sample matrixmechanic force mechanic force compounding resistance rise spinning Nos.powder (wt. %) (wt. %) powdermixer) (Ω/sq) (ΔPa/min ) ability C-PBT C.Ex. 1   0% — — >10¹³ <2 Pa/20 min — PCN3-0 C. Ex. 2 3.00% — w/o 2 ×10⁴ >90 Pa/8 min Very poor PCN6-1 C. Ex. 3 6.00% — w/o 4 × 10² >150 Pa/9min Very poor PCN6-2 C. Ex. 4 6.00% — w 3 × 10² >50 Pa/10 min Very poorPCN6-3 C. Ex. 5 —  6.00% w difficult to granulate PCN1-1 Ex. 1 —  1.00%w 1 × 10⁸ <2 Pa/20 min excellent PCN3-1 Ex. 2 —  3.00% w 8 × 10³ <10Pa/70 min good PCN6-4 Ex. 3 —  6.00% w 2 × 10² <10 Pa/50 min good PCN6-5Ex. 4 —  6.00% w 1 × 10² <5 Pa/100 min good PCN8-5 Ex. 5 —  8.00% w 6 ×10¹ <10 Pa/90 min good PCN10-1 Ex. 6 — 10.00% w 7 <10 Pa/50 min good

In overall, the lower the rise pressure is, the better the distributionof the carbon nanotube in PBT polyester matrix is. As shown on theresult of table 2, the conductive masterbatches (such as PCN3-0 andPCN6-1) formed from polyester matrix powder which contains carbonnanotube which is dispersed without using a high-speed, highly strongmechanic force has a higher pressure rise and exhibits poor spinningability. The conductive masterbatches (PCN6-2) formed from PBT polyestermatrix powder dispersed with a high-speed, highly strong mechanic forceand then granulated has a lower pressure rise but poor spinning ability.Further, if the PBT matrix powder contains no chain extenders, theconductive masterbatches (such as PCN6-3) formed therefrom are difficultto granulate or cannot be granulated.

In contrast, according to the present invention, the conductivemasterbatches (such as PCN3-1, PCN6-4, PCN6-5, PCN8-5 and PCN10-1)formed from the PBT polyester matrix powder which contains ahomogeneously dispersed carbon nanotube, a dispersant and a chainextender have lower pressure rise and exhibit better spinning ability.

The conductive resistance is tested for the conductive masterbatchesformed from the PBT matrix powders which are prepared by the aboveExamples and Comparative Examples and the results are shown on table 2.

As shown on table 2, the surface resistance of the conductivemasterbatches according to the present invention, which is formed fromthe PBT polyester matrix powder containing a homogeneously dispersedcarbon nanotube, a dispersant and a chain extender, are decreased as thecontent of the carbon nanotube is increased. Namely, it appears that theconductivity of the conductive masterbatches is increased as the contentof the carbon nanotube is increased. On the other side, as compared withthe masterbatches (C-PBT) prepared from a pure PBT polyester matrixpowder, the conductive masterbatches (such as PCN3-1, PCN6-4, PCN6-5,PCN8-5 and PCN10-1) formed from the PBT polyester powder according tothe present invention have a significantly increased conductivity. Inaddition, as compared with the conductive masterbatches prepared fromthe PBT matrix powder containing the same amount of carbon nanotubedispersed without the use of a high-speed, highly mechanical force (suchas PCN6-1, PCN6-2) or from the PBT matrix powder containing no chainextenders (such as PCN6-3), the conductive masterbatches (such asPCN6-4, PCN6-5) according to the present invention exhibit betterconductivity and lower surface resistance.

C. Preparation and Property Test of the Conductive PBT Monofilament

The conductive masterbatches, C-PBT, PCN1-1, PCN3-1, PCN6-4, PCN6-5,PCN8-5 and PCN10-1, are baked and dried at a temperature of 1100 over aperiod of 12 hours to obtain dried conductive masterbatches. The driedconductive masterbatches are fed into a single-screw extruder, and areextruded at a processing temperature of 250 to 285° C. and at a screwspeed of 20 rpm through a 60 μm of filtering screen and then are spunthrough a spinning nozzle with a pore diameter of 0.5 mm and a length of1 mm at a single pore extruding output of 6 g/minutes. After that, thespun filaments are cooled by a cooling device at a cooling speed of 5 to30 m/minutes and then winded at a winding speed of 40 to 100 m/minutes.After the cooling and crimping procedures, the conductive monofilaments(Nos.: F-PBT, F-PCN1-1, F-PCN3-1, F-PCN6-4, F-PCN6-5, F-PCN8-5 andF-PCN10-1) are formed.

The conductivity, tension, strength and elongation of the thus-preparedconductive monofilaments are determined and the result is shown on table3.

TABLE 3 Volume Content specific Conductive PBT of carbon Fiberresistance Surface Sample masterbatches matrix nanotube, diameter Denierof fiber resistance Tension Strength elongation Nos. Nos. powder wt. %(mm) (D) (Ω · cm) (Ω/sq) (Kg) (gf/d) (%) F-PBT C-PBT C. Ex. 1 0 0.27 698— — 1.47 2.1 100 F-PCN1-1 PCN1-1 Ex. 1 1 0.25 600 — 10⁹ 0.83 1.4 80F-PCN3-1 PCN3-1 Ex. 2 3 0.24 552 3.3 × 10³ 10⁵ 0.73 1.3 60 F-PCN6-4PCN6-4 Ex. 3 6 0.26 648 1.6 × 10² 10^(3~4) 0.753 1.1 35 F-PCN6-5 PCN6-5Ex. 4 6 0.28 751 3.6 × 10² 10^(3~4) 0.8 1.1 37 F-PCN8-5 PCN8-5 Ex. 5 80.205 403 26 10³ 0.562 1.3 18 F-PCN10-1 PCN10-1 Ex. 6 10 0.205 403 1210²⁻³ 0.58 1.44 19

As shown on table 3, the conductive monofilaments prepared fromconductive masterbatches formed by polybutylene terephthalate polymericmatrix powders which respectively contain 3%, 6%, 8% and 10% ofdispersed carbon nanotube powders have a better conductivity in a rangeof up to 10² to 10⁵ Ω/sq. As compared with the monofilament (F-PBT)prepared from a pure polybutylene terephthalate masterbatches, themonofilaments prepared from the conductive masterbatches according tothe present invention have better tension and stable strength.

While the embodiments of the present invention described herein arepresently preferred, various modifications and improvements can be madewithout departing from the spirit and scope of the present invention.The scope of the present invention is indicated by the appended claims,and all changes that fall within the meaning and range of equivalentsare intended to be embraced therein.

What is claimed is:
 1. A polyester matrix powder containing ahomogeneously dispersed carbon nanotube powder, comprising: A) 80 to99.5 wt. % of a polyester polymeric matrix based on a polybutyleneterephthalate (PBT) or the copolymer thereof, based on the weight ofpolyester matrix powder, B) 1 to 15 wt. % of a carbon nanotube powdermilled at ultrahigh speed, based on the weight of polyester matrixpowder, C) 0.01 to 6.0 wt. % of a dispersant, based on the weight ofpolyester matrix powder, D) 0.01 to 6.0 wt. % of a chain extender, basedon the weight of polyester matrix powder; wherein components A), B), C)and D) are mixed by means of a high-speed powder mixer to obtain apolyester matrix powder; wherein the chain extender is selected from thegroup consisting of a diisocyanatocycloalkane and an oxazoline; whereinthe oxazoline is selected from the group consisting of adiisocyanatocyclohexane, a bis-oxazoline, 1,4-phenylene bis-oxazoline,2,2′-methylene[(4,s)-4-tert-butyle-2-oxazoline] and2,2′-methylene[(4,s)-4-phenyl-2-oxazoline].
 2. The polyester matrixpowder according to claim 1, wherein the polybutylene terephthalate orthe copolymer thereof in component A) is selected from the groupconsisting of a polybutylene terephthalate homopolymer, a copolyesterhaving a repeat unit of butylene terephthalate (BT) and a blockcopolymer having a unit of polybutylene terephthalate, and thecombination thereof.
 3. The polyester matrix powder according to claim2, wherein the polyester polymeric matrix is based on a polybutyleneterephthalate homopolymer.
 4. The polyester matrix powder according toclaim 1, wherein the polybutylene terephthalate or the copolymer thereofhas an intrinsic viscosity (I.V.) of more than 0.6 dl/g.
 5. Thepolyester matrix powder according to claim 4, wherein the polybutyleneterephthalate or the copolymer thereof has an intrinsic viscosity (I.V.)in a range of 0.6 to 1.3 dl/g.
 6. The polyester matrix powder accordingto claim 5, wherein the polybutylene terephthalate or the copolymerthereof has an intrinsic viscosity (I.V.) in a range of 0.8 to 1.3 dl/g.7. The polyester matrix powder according to claim 1, wherein thepolyester polymeric matrix is in an amount of 84 to 99 wt. %, based onthe weight of polyester matrix powder.
 8. The polyester matrix powderaccording to claim 7, wherein the polyester polymeric matrix is in anamount of 88 to 97 wt. %, based on the weight of polyester matrixpowder.
 9. The polyester matrix powder according to claim 1, wherein thecarbon nanotube powder prepared via ultrahigh-speed milling has a length(L) of less than 3.0 μm and an L/D value of more than
 100. 10. Thepolyester matrix powder according to claim 1, wherein the milled carbonnanotube powder has a length (L) of 0.7 to 3.0 μm and an L/D value of100 to
 300. 11. The polyester matrix powder according to claim 1,wherein the milled carbon nanotube powder is formed from a carbonnanotube with an average tube diameter of 0.5 to 50 nm (nanometer) orwith an L/D value of 60 to
 600. 12. The polyester matrix powderaccording to claim 1, wherein component B) is in amount of 1 to 10 wt.%, based on the weight of polyester matrix powder.
 13. The polyestermatrix powder according to claim 12, wherein component B) is in anamount of 2.5 to 10 wt. %, based on the weight of polyester matrixpowder.
 14. The polyester matrix powder according to claim 13, whereincomponent B) is in an amount of 3 to 10 wt. %, based on the weight ofpolyester matrix powder.
 15. The polyester matrix powder according toclaim 1, wherein the dispersant is an ethylene-acrylic copolymer. 16.The polyester matrix powder according to claim 15, wherein thedispersant is ethylene-acrylic acid copolymer.
 17. The polyester matrixpowder according to claim 1, wherein the dispersant is in an amount of0.1 to 2.0 wt. %, based on the weight of polyester matrix powder. 18.The polyester matrix powder according to claim 17, wherein thedispersant is in an amount of 0.2 to 1.5 wt. %, based on the weight ofpolyester matrix powder.
 19. The polyester matrix powder according toclaim 1, wherein the oxazoline is2,2′-methylene[(4,s)-4-tert-butyle-2-oxazoline] or2,2′-methylene[(4,s)-4-phenyl-2-oxazoline].
 20. The polyester matrixpowder according to claim 1, wherein the chain extender is in an amountof 0.1 to 1.0 wt. %, based on the weight of polyester matrix powder. 21.The polyester matrix powder according to claim 20, wherein the chainextender is in an amount of 0.1 to 0.8 wt. %, based on the weight ofpolyester matrix powder.
 22. Conductive masterbatches, which areprepared from the polyester matrix powder according to claim
 1. 23. Theconductive masterbatches according to claim 22, wherein the resistanceof conductive masterbatches is in a range of 10⁰ to 10⁸ Ω/sq.
 24. Theconductive masterbatches according to claim 23, wherein the resistanceof conductive masterbatches is in a range of 10⁰ to 10⁵ Ω/sq.
 25. Aconductive monofilament, which is formed from the conductivemasterbatches according to claim
 22. 26. The conductive monofilamentaccording to claim 25, wherein the fiber diameter of the conductivemonofilament is in a range of 0.05 to 1.0 mm.
 27. The conductivemonofilament according to claim 26, wherein the fiber diameter of theconductive monofilament is in a range of 0.1 to 0.5 mm.
 28. Theconductive monofilament according to claim 25, wherein the conductivemonofilament has a volume resistance in a range of 10⁴ Ω·cm or less, astrength of 0.8 gf/d or more and an elongation of 10% or more.
 29. Theconductive monofilament according to claim 28, wherein the conductivemonofilament has a volume resistance in a range of 10¹ to 10³ Ω·cm, astrength of 1.0 to 4.0 gf/d and an elongation of 10 to 70%.
 30. Textilescomprising the monofilament according to claim
 25. 31. The textilesaccording to claim 30, wherein the textiles have a surface resistance ofless than 10⁵ Ω/sq.
 32. The textiles according to claim 31, wherein thetextiles have a surface resistance of 10¹ to 10⁵ Ω/sq.
 33. A process forthe preparation of a conductive monofilament comprising the steps: 1)providing conductive masterbatches, 2) placing the conductivemasterbatches at a temperature of 110 ° C. and baking over a period of 6to 30 hours to obtain dried conductive masterbatches, 3) feeding thedried conductive masterbatches into a single screw extruder andextruding at a processing temperature of 250 to 285° C. and at a screwspeed of 20 rpm, and then extruding through a filter with 60 μm screen,followed by spinning via a spinning nozzle with a pore diameter of 0 5mm and a length of 1 mm to obtain a spun filament, 4) cooling the spunfilament from step (3) at a cooling rate of 5 to 30 m/min through acooling device and then winding at a winding rate of 40 to 100 m/min toform a conductive monofilament; wherein the conductive masterbatches areprepared from a polyester matrix powder containing a homogeneouslydispersed carbon nanotube powder, comprising: A) 80 to 99.5 wt. % of apolyester polymeric matrix based on a polybutylene terephthalate (PBT)or the copolymer thereof, based on the weight of polyester matrixpowder, B) 1 to 15 wt. % of a carbon nanotube powder milled at ultrahighspeed, based on the weight of polyester matrix powder, C) 0.01 to 6.0wt. % of a dispersant, based on the weight of polyester matrix powder,D) 0.01 to 6.0 wt. % of a chain extender, based on the weight ofpolyester matrix powder, wherein components A), B), C) and D) are mixedby means of a high-speed powder mixer to obtain a polyester matrixpowder.